EP0037015A2 - Process for the preparation of 2-chloro-acetoacetic acid esters - Google Patents

Process for the preparation of 2-chloro-acetoacetic acid esters Download PDF

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Publication number
EP0037015A2
EP0037015A2 EP81102029A EP81102029A EP0037015A2 EP 0037015 A2 EP0037015 A2 EP 0037015A2 EP 81102029 A EP81102029 A EP 81102029A EP 81102029 A EP81102029 A EP 81102029A EP 0037015 A2 EP0037015 A2 EP 0037015A2
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Prior art keywords
chloride
temperatures
chloroacetoacetic
acid esters
preparation
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EP81102029A
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German (de)
French (fr)
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EP0037015B1 (en
EP0037015A3 (en
Inventor
René Dr. Blum
Leander Dr. Tenud
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Lonza AG
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Lonza AG
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/46Preparation of carboxylic acid esters from ketenes or polyketenes

Definitions

  • the present invention relates to a process for the preparation of 2-chloroacetoacetic acid esters.
  • 2-Chloroacetoacetic acid esters can be used for the preparation of coumaric acid derivatives, which are known as an intermediate for the production of crop protection agents.
  • 2-chloroacetoacetic acid esters are also intermediates for pharmaceutical preparations, e.g. Cimetidine.
  • the chlorination with sulfuryl chloride proceeds up to high conversions with a good yield (93-97%), but has the disadvantage that the gases generated during the reaction, S0 2 and HCl, have to be separated and the sulfur dioxide in again in a special work process the sulfuryl chloride must be converted.
  • the aim of the present invention is a simple, powerful method. According to the invention, this is achieved by starting from diketene, this at temperatures from +10 to -40 ° C in the presence of chlorinated aliphatic hydrocarbon preferably with 1 to 3 carbon atoms as a solvent with HC1 in the acetoacetic acid chloride, by introducing chlorine at temperatures of ⁇ 10 to -40 ° C forms the 2-chloroacetoacetic acid chloride and the latter converted into the corresponding ester by adding preferably aliphatic alcohols having 1 to 4 carbon atoms.
  • the chlorination can be carried out in the presence of acidic catalysts such as Lewis acids, for example PC1 3 , FeC1 3 , inorganic acids, for example sulfuric acid, perchloric acid, or strong organic carboxylic acids, for example acetic acid, trifluoroacetic acid, p-toluenesulfonic acid.
  • acidic catalysts such as Lewis acids, for example PC1 3 , FeC1 3 , inorganic acids, for example sulfuric acid, perchloric acid, or strong organic carboxylic acids, for example acetic acid, trifluoroacetic acid, p-toluenesulfonic acid.
  • Chlorinated aliphatic hydrocarbons such as carbon tetrachloride, ethyl chloride, dichloroethane, etc., preferably methylene chloride, are used as solvents.
  • solvents such as carbon tetrachloride, ethyl chloride, dichloroethane, etc., preferably methylene chloride.
  • 200 to 1000 g of solvent are used per mole of diketene.
  • the molar ratio of HC1 to diketene in the first stage can vary widely, expediently 1.1 to 10 mol, preferably 1.95 to 6.5 mol, of HCl are used per mol of diketene.
  • 0.9 to 1.1 moles of chlorine are preferably used per mole of acetoacetic acid chloride.
  • the 2-chloroacetoacetic acid chloride obtained in the second stage is reacted with the appropriate alcohol with 1 to 4 carbon atoms implemented in a third stage.
  • alcohols are methyl, ethyl, propyl, butyl alcohol.
  • the amount of alcohol to be added is the stoichiometric amount. In some cases it may be appropriate to use a slight excess, advantageously from 0.1 to 0.3 mol.
  • a particularly preferred embodiment of the invention consists in that the three stages can be carried out in the same reaction medium and reaction vessel without having to isolate one of the intermediates.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

1. Process for the production of 2-chloroacetoacetic esters, characterized in converting diketene at temperatures of from +10 to -40 degrees C in the presence of chlorinated aliphatic hydrocarbons as solvent by using hydrogen chloride into the acetoacetic chloride, forming the 2-chloroacetoacetic chloride by introducing of chlorine at temperature of from +10 to -40 degrees C, and converting the 2-chloroacetoacetic chloride by adding of alcohols having from 1 to 4 carbon atoms at temperatures of from +10 to -40 degrees C into the corresponding esters.

Description

Die vorliegende Erfindung betrifft ein Verfahren zur Herstellung von 2-Chloracetessigsäureestern. 2-Chloracetessigsäureester können zur Herstellung von Cumarilsäurederivaten verwendet werden, die als Zwischenprodukt zur Herstellung von Pflanzenschutzmitteln bekannt sind. 2-Chloracetessigsäureester stellen auch Zwischenprodukte für pharmazeutische Präparate, z.B. Cimetidin, dar.The present invention relates to a process for the preparation of 2-chloroacetoacetic acid esters. 2-Chloroacetoacetic acid esters can be used for the preparation of coumaric acid derivatives, which are known as an intermediate for the production of crop protection agents. 2-chloroacetoacetic acid esters are also intermediates for pharmaceutical preparations, e.g. Cimetidine.

Bei den bisher bekannten Herstellungsverfahren wird von Acetessigsäureestern ausgegangen, die entweder mit Sulfurylchlorid oder mit Chlor chloriert werden.The previously known production processes are based on acetoacetic acid esters, which are chlorinated either with sulfuryl chloride or with chlorine.

Die Chlorierung mit Sulfurylchlorid verläuft zwar bis zu hohen Umsätzen mit guter Ausbeute (93-97%), hat jedoch den Nachteil, dass die bei der Reaktion entstehenden Gase, S02 und HCl, getrennt werden müssen und das Schwefeldioxid in einem speziellen Arbeitsprozess wieder in das Sulfurylchlorid umgewandelt werden muss.The chlorination with sulfuryl chloride proceeds up to high conversions with a good yield (93-97%), but has the disadvantage that the gases generated during the reaction, S0 2 and HCl, have to be separated and the sulfur dioxide in again in a special work process the sulfuryl chloride must be converted.

Bei der Chlorierung von Acetessigestern mit Chlor können, wenn die Reaktion kontinuierlich durchgeführt wird, relativ gute Selektivitäten und Ausbeuten erreicht werden (DE-OS 27 09 138).In the chlorination of acetoacetic esters with chlorine, if the reaction is carried out continuously, relatively good selectivities and yields can be achieved (DE-OS 27 09 138).

Ziel der vorliegenden Erfindung ist ein einfaches, leistungsfähiges Verfahren. Erfindungsgemäss wird dies dadurch erreicht, dass man von Diketen ausgeht, dieses bei Temperaturen von +10 bis -40°C in Gegenwart von chloriertem aliphatischen Kohlenwasserstoff vorzugsweise mit 1 bis 3 Kohlenstoffatomen als Lösungsmittel mit HC1 in das Acetessigsäurechlorid überführt, durch Einleiten von Chlor bei Temperaturen von ±10 bis -40°C das 2-Chloracetessigsäurechlorid bildet und letzteres durch Zugabe von vorzugsweise aliphatischen Alkoholen mit 1 bis 4 C-Atomen in den entsprechenden Ester überführt.The aim of the present invention is a simple, powerful method. According to the invention, this is achieved by starting from diketene, this at temperatures from +10 to -40 ° C in the presence of chlorinated aliphatic hydrocarbon preferably with 1 to 3 carbon atoms as a solvent with HC1 in the acetoacetic acid chloride, by introducing chlorine at temperatures of ± 10 to -40 ° C forms the 2-chloroacetoacetic acid chloride and the latter converted into the corresponding ester by adding preferably aliphatic alcohols having 1 to 4 carbon atoms.

Die Chlorierung kann in Gegenwart von sauren Katalysatoren, wie Lewis-Säuren, z.B. PC13, FeC13, anorganischen Säuren, z.B. Schwefelsäure, Perchlorsäure, oder starken organischen Carbonsäuren, z.B. Essigsäure, Trifluoressigsäure, p-Toluolsulfonsäure, durchgeführt werden. Diese Säuren werden in katalytischen Mengen, zweckmässig 0,1 bis 20 Mol%, bezogen auf eingesetztes Diketen, zugesetzt.The chlorination can be carried out in the presence of acidic catalysts such as Lewis acids, for example PC1 3 , FeC1 3 , inorganic acids, for example sulfuric acid, perchloric acid, or strong organic carboxylic acids, for example acetic acid, trifluoroacetic acid, p-toluenesulfonic acid. These acids are added in catalytic amounts, advantageously 0.1 to 20 mol%, based on the diketene used.

Als Lösungsmittel werden chlorierte aliphatische Kohlenwasserstoffe, wie Tetrachlorkohlenstoff, Aethylchlorid, Dichloräthan usw., vorzugsweise Methylenchlorid, verwendet. Zweckmässig setzt man pro Mol Diketen 200 bis 1000'g Lösungsmittel ein.Chlorinated aliphatic hydrocarbons such as carbon tetrachloride, ethyl chloride, dichloroethane, etc., preferably methylene chloride, are used as solvents. Appropriately, 200 to 1000 g of solvent are used per mole of diketene.

Das Molverhältnis HC1 zu Diketen in der ersten Stufe kann stark variieren, zweckmässig wird pro Mol Diketen 1,1 bis 10 Mol, vorzugsweise 1,95 bis 6,5 Mol HCl, angewendet.The molar ratio of HC1 to diketene in the first stage can vary widely, expediently 1.1 to 10 mol, preferably 1.95 to 6.5 mol, of HCl are used per mol of diketene.

Für die Chlorierung mit Chlor in der zweiten Stufe werden vorzugsweise pro Mol Acetessigsäurechlorid 0,9 bis 1,1 Mol Chlor angewendet.For chlorination with chlorine in the second stage, 0.9 to 1.1 moles of chlorine are preferably used per mole of acetoacetic acid chloride.

Zur Herstellung der gewünschten Ester wird das in der zweiten Stufe erhaltene 2-Chloracetessigsäurechlorid mit dem entsprechenden Alkohol mit 1 bis 4 C-Atomen in einer dritten Stufe umgesetzt. Solche Alkohole sind Methyl-, Aethyl-, Propyl-, Butylalkohol.To produce the desired esters, the 2-chloroacetoacetic acid chloride obtained in the second stage is reacted with the appropriate alcohol with 1 to 4 carbon atoms implemented in a third stage. Such alcohols are methyl, ethyl, propyl, butyl alcohol.

Die hinzuzusetzende Menge an Alkohol sind die stöchiometrischen Mengen. Es kann in manchen Fällen zweckmässig sein, einen leichten Ueberschuss, zweckmässig von 0,1 bis 0,3 Mol, anzuwenden.The amount of alcohol to be added is the stoichiometric amount. In some cases it may be appropriate to use a slight excess, advantageously from 0.1 to 0.3 mol.

Eine besonders bevorzugte Ausführungsform der Erfindung besteht darin, dass man die drei Stufen im selben Reaktionsmedium und Reaktionsgefäss, ohne dass eines der Zwischenprodukte isoliert werden muss, durchführen kann.A particularly preferred embodiment of the invention consists in that the three stages can be carried out in the same reaction medium and reaction vessel without having to isolate one of the intermediates.

Beispiel 1example 1

In einem Doppelmantelkolben von 500 ml Grösse, ausgestattet mit Pressluftrührer, Thermometer, Gaseinleitungsrohr mit Fritte, Rückflusskühler und Kryomat, wurden 50,45 g (0,6 Mol) Diketen in 300 ml Methylenchlorid gelöst und auf -20oC abgekühlt. Nach Zusatz von 0,11 Mol% H2S04, bezogen auf Diketen, und 43,8 g (1,2 Mol) Chlorwasserstoff, bezogen auf Diketen, wurden nach 3 1/2 Stunden Rühren während 35 Minuten 42,5 g (0,6 Mol) Chlor eingeleitet und weitere 30 Minuten gerührt. Anschliessend wurde immer noch bei -20 bis -10°C 27,6 g (0,6 Mol) absoluter Aethanol zugetropft und während 15 Minuten gerührt.Equipped with Pressluftrührer, thermometer, gas inlet tube with frit, reflux condenser and Kryomat in a jacketed flask of 500 ml size, 50.45 g (0.6 mol) of diketene were dissolved in 300 ml of methylene chloride and cooled to -20 ° C. After adding 0.11 mol% of H 2 SO 4 , based on diketene, and 43.8 g (1.2 mol) of hydrogen chloride, based on diketene, 42.5 g (after 35 minutes stirring) were added for 35 minutes. 0.6 mol) chlorine introduced and stirred for a further 30 minutes. Subsequently, 27.6 g (0.6 mol) of absolute ethanol were still added dropwise at -20 to -10 ° C. and the mixture was stirred for 15 minutes.

Anschliessend wurde das-Lösungsmittel am Rotavap abgedampft. Es resultierten 98,7 g 2-Chloracetessigsäure- äthylester mit einem Gehalt von 83,4 Gew.%.The solvent was then evaporated off on a Rotavap. The result was 98.7 g of ethyl 2-chloroacetoacetate with a content of 83.4% by weight.

Beispiele 2 - 6Examples 2-6

Nachstehende Tabelle zeigt die Ergebnisse weiterer Versuche.

Figure imgb0001
The table below shows the results of further tests.
Figure imgb0001

Claims (4)

1. Verfahren zur Herstellung von 2-Chloracetessigsäureestern, dadurch gekennzeichnet, dass man Diketen bei Temperaturen von +10 bis -40°C in Gegenwart von chlorierten aliphatischen Kohlenwasserstoffen als Lösungsmittel mit Hilfe von Chlorwasserstoff in das Acetessigsäurechlorid überführt, durch Einleiten von Chlor bei Temperaturen von +10 bis -40°C das 2-Chloracetessigsäurechlorid bildet und letzteres durch Zugabe von Alkoholen mit 1 bis 4 C-Atomen bei Temperaturen von +10 bis -40oC in den entsprechenden Ester überführt.1. A process for the preparation of 2-chloroacetoacetic acid esters, characterized in that diketene at temperatures from +10 to -40 ° C in the presence of chlorinated aliphatic hydrocarbons as a solvent with the aid of hydrogen chloride in the acetoacetic acid chloride, by introducing chlorine at temperatures of +10 to -40 ° C forms the 2-chloroacetoacetic acid chloride and the latter is converted into the corresponding ester by adding alcohols with 1 to 4 C atoms at temperatures of +10 to -40 o C. 2. Verfahren nach Patentanspruch l, dadurch gekennzeichnet, dass man die Chlorierung in Gegenwart von sauren Katalysatoren durchführt.2. The method according to claim 1, characterized in that the chlorination is carried out in the presence of acidic catalysts. 3. Verfahren nach Patentansprüchen 1 und 2, dadurch gekennzeichnet, dass man als Lösungsmittel Methylenchlorid verwendet.3. The method according to claims 1 and 2, characterized in that methylene chloride is used as the solvent. 4. Verfahren nach einem oder mehreren der Patentansprüche 1 - 3, dadurch gekennzeichnet, daß man die Dreistufenreaktion ohne Isolierung der Zwischenproduckte durchführt.4. The method according to one or more of claims 1-3, characterized in that one carries out the three-stage reaction without isolation of the intermediates.
EP81102029A 1980-04-02 1981-03-18 Process for the preparation of 2-chloro-acetoacetic acid esters Expired EP0037015B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT81102029T ATE3852T1 (en) 1980-04-02 1981-03-18 PROCESS FOR THE PREPARATION OF 2CHLORACETETTINE[UREESTERS.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CH2606/80 1980-04-02
CH260680 1980-04-02

Publications (3)

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EP0037015A2 true EP0037015A2 (en) 1981-10-07
EP0037015A3 EP0037015A3 (en) 1981-12-30
EP0037015B1 EP0037015B1 (en) 1983-06-22

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EP (1) EP0037015B1 (en)
JP (1) JPS56154438A (en)
AT (1) ATE3852T1 (en)
CS (1) CS217995B2 (en)
DD (1) DD157794A5 (en)
DE (1) DE3160460D1 (en)
IN (1) IN151753B (en)
MX (1) MX152284A (en)
PL (1) PL134443B1 (en)
SU (1) SU988187A3 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0061657A1 (en) * 1981-03-26 1982-10-06 Lonza Ag Process for the preparation of 2-chloracetoacetamides
US8859786B2 (en) 2011-04-01 2014-10-14 Lonza Ltd Preparation of 3,5-dioxo hexanoate ester in two steps
WO2017093214A1 (en) 2015-12-03 2017-06-08 Bayer Cropscience Aktiengesellschaft Mesoionic halogenated 3-(acetyl)-1-[(1,3-thiazol-5-yl)methyl]-1h-imidazo[1,2-a]pyridin-4-ium-2-olate derivatives and related compounds as insecticides
WO2018229202A1 (en) 2017-06-16 2018-12-20 Basf Se Mesoionic imidazolium compounds and derivatives for combating animal pests
CN109503381A (en) * 2018-12-12 2019-03-22 安徽金禾实业股份有限公司 4- chloroacetyl acetacetic ester microchannel plate induction method and device
CN113877504A (en) * 2021-11-03 2022-01-04 江苏恒安化工有限公司 Preparation device and method of ethyl 4-chloroacetoacetate

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6025955A (en) * 1983-07-22 1985-02-08 Nippon Synthetic Chem Ind Co Ltd:The Production of gamma-chloroacetoacetic acid ester

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2209683A (en) * 1936-06-27 1940-07-30 Carbide & Carbon Chem Corp Halogenation of diketene
US3666793A (en) * 1968-04-24 1972-05-30 Lonza Ag Process for the production of {65 -chloroacetoacetic acid esters
JPS51113824A (en) * 1975-03-27 1976-10-07 Nippon Synthetic Chem Ind Co Ltd:The Preparation of gamma-chloroacetoacetyl chloride

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2209683A (en) * 1936-06-27 1940-07-30 Carbide & Carbon Chem Corp Halogenation of diketene
US3666793A (en) * 1968-04-24 1972-05-30 Lonza Ag Process for the production of {65 -chloroacetoacetic acid esters
JPS51113824A (en) * 1975-03-27 1976-10-07 Nippon Synthetic Chem Ind Co Ltd:The Preparation of gamma-chloroacetoacetyl chloride

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
CHEMICAL ABSTRACTS, Band 34, Nr. 18, 20-09-1940, spalte 62228 Columbus, Ohio, US C.D. HURD et al.: "Chlorination and Structure of Acetylketene" & J. Am. Chem. Soc. 62, 1147-8 (1940) * insgesamt * *
CHEMICAL ABSTRACTS, Band 46, Nr. 17, 10-09-1952, spalte 8115c Columbus, Ohio, US V.V. PEREKALIN et al.: "Reactions of Diketene. Reaction of Diketene with some Weakly Basic Aromatic Amines" & Zhur. Obshchei. Khim. 21, 1995-2001 (1951) * insgesamt * *
CHEMICAL ABSTRACTS, Band 86, Nr. 19. 09-05-1977, seite 506, Zusammenfassung 139408h Columbus, Ohio, US & JP-A-51 113 824 (Nippon Synthetic Chemical Industry) (27-03-1975) * insgesamt * *
Chemische Berichte, Band 81, Nr. 5 Oktober 1948, Berlin, DE H. BRINTZINGER et al.: "Notiz Uber Thioketone", seiten 380,381 * Insgesamt * *

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0061657A1 (en) * 1981-03-26 1982-10-06 Lonza Ag Process for the preparation of 2-chloracetoacetamides
US4801750A (en) * 1981-03-26 1989-01-31 Lonza Ltd. Process for the produciton of 2-chloroacetoacetic acid amides
US8859786B2 (en) 2011-04-01 2014-10-14 Lonza Ltd Preparation of 3,5-dioxo hexanoate ester in two steps
US9296718B2 (en) 2011-04-01 2016-03-29 Lonza Ltd Preparation of 3,5-dioxo hexanoate ester in two steps
WO2017093214A1 (en) 2015-12-03 2017-06-08 Bayer Cropscience Aktiengesellschaft Mesoionic halogenated 3-(acetyl)-1-[(1,3-thiazol-5-yl)methyl]-1h-imidazo[1,2-a]pyridin-4-ium-2-olate derivatives and related compounds as insecticides
WO2018229202A1 (en) 2017-06-16 2018-12-20 Basf Se Mesoionic imidazolium compounds and derivatives for combating animal pests
CN109503381A (en) * 2018-12-12 2019-03-22 安徽金禾实业股份有限公司 4- chloroacetyl acetacetic ester microchannel plate induction method and device
CN109503381B (en) * 2018-12-12 2022-04-29 安徽金禾实业股份有限公司 4-chloroacetoacetic acid ethyl ester microchannel reaction method and device
CN113877504A (en) * 2021-11-03 2022-01-04 江苏恒安化工有限公司 Preparation device and method of ethyl 4-chloroacetoacetate

Also Published As

Publication number Publication date
JPS56154438A (en) 1981-11-30
EP0037015B1 (en) 1983-06-22
SU988187A3 (en) 1983-01-07
DE3160460D1 (en) 1983-07-28
MX152284A (en) 1985-06-20
DD157794A5 (en) 1982-12-08
PL134443B1 (en) 1985-08-31
IN151753B (en) 1983-07-23
ATE3852T1 (en) 1983-07-15
PL230340A1 (en) 1981-11-27
JPH0125735B2 (en) 1989-05-19
EP0037015A3 (en) 1981-12-30
CS217995B2 (en) 1983-02-25

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